Method of treating fluids

ABSTRACT

A method for treating fluid to remove hydrogen sulfide and sulfur dioxide is disclosed. The method includes passing fluid containing the hydrogen sulfide and/or sulfur dioxide through a bed of metal particulate matter. The metal particulate matter is preferably chosen from metals having favorable redox potentials relative to the redox potentials of these undesirable constituents so as to establish conditions for spontaneous oxidation and reduction reactions between the undesirable constituents and the metal particles.

This application is a continuation of Ser. No. 685,159, filed Apr. 12,1991, now U.S. Pat. No. 5,122,274, which is a continuation of Ser. No.07/425,370, filed Oct. 17, 1989, now abandoned, which is a continuationof Ser. No. 154,522, filed Feb. 11, 1988, now abandoned, which is acontinuation of 06/911,392, filed Sep. 25, 1986, now abandoned, which isa continuation-in-part of 06/605,652, filed Apr. 30, 1984, nowabandoned.

BACKGROUND AND DESCRIPTION OF THE INVENTION

The present invention generally relates to fluid treating and, moreparticularly, to methods which are especially adapted for providing forimproved treatment of fluids. Although capable of a variety of uses,this invention finds advantageous utility in the treatment of water toremove undesirable constituents contained therein such as, for example,dissolved chlorine and nitrates constituents.

In the field of fluid treating, and particularly in the field oftreating water for commercial, industrial and domestic use, a number ofsystems have been proposed, some or all of which have certainundesirable characteristics, drawbacks or disadvantages associatedtherewith.

For example, ion-exchange systems are commonly used to soften water andselectively remove specific impurities from the water. The active mediumof the ion-exchanger is an ion-exchange resin which is designed toremove undesirable constituents from the fluid and replace thoseundesirable constituents with a less undesirable constituent. Forinstance, a cation exchange resin employed to remove thehardness-producing elements of calcium and magnesium may be designed tosimultaneously give up sodium in exchange for the calcium and magnesiumcontained in the water which has passed through the ion-exchanger.Regardless of the specific ion-exchange resin used, eventually the bedof resin becomes exhausted and the unit must be removed from service andbe regenerated to become useful again. In addition to exhaustion theresin is also susceptible to chemical degradation. Accordingly, theion-exchanger unit must be carefully maintained and monitored to assurecontinued acceptable performance.

Another popular type of process for treating water is reverse osmosiswherein pressure in excess of the osmotic pressure of the fluid is usedto force untreated water, normally at ambient temperature, through aselective membrane in a direction opposite to that normally observed inosmotic processes. The selective membrane is designed to allow the waterto permeate through while rejecting the dissolved undesirableconstituents. The success of this process depends in large part upon thedevelopment of suitable membranes. Membranes utilized in reverse osmosistypically experience a variety of temperature, chemical and pressurestability problems as well as speed and capacity limitations. Forexample, water supplies are commonly treated with chlorine as anantibacterial agent. The dissolved chlorine, although highly effectivein combating bacteria, often has a deleterious effect on reverse osmosismembranes. Additionally, reverse osmotic equipment also must becarefully set up, maintained, and monitored. Accordingly, regardless ofthe sophistication of the technology used, if the end user fails tomaintain the system and perform the necessary sampling required toensure that the system is functioning to design specifications abreakdown in treatment can occur.

Still another popular water treatment process is the application ofactivated carbon, which is widely used for taste and odor control aswell as removal of organic contaminants from water by adsorbtion sinceactivated carbon is characterized by a high adsorbtivity for gases,vapors, and colloidal solids. However, similiar to the resin inion-exchangers, the adsorbtive capacity of the carbon is eventuallydepleted and the carbon either must be regenerated or replaced.Therefore a system incorporating activated carbon also requires carefulmonitoring to determine the effectiveness of the medium.

Hydrogen sulfide is normally removed from water by chlorination.Unfortunately, this requires the subsequent stop of removing thechlorine which can be accomplished by the use of activated carbon. Againthe activated carbon is eventually depleted and the carbon must beregenerated or replaced. Use of the present process eliminates the needfor this procedure.

The present invention overcomes the undesirable characteristics,drawbacks and disadvantages of the prior art by providing a fluidtreating method which employs metal particulate matter having a redoxpotential which relative to the redox potential of the undesirableconstituents sought to be treated favors spontaneous oxidation-reductionreactions between the metal and the undesirable constituents. The metalparticulate matter can be of varying mesh size, preferably of from 4 to30 mesh based on U.S. Standard screen sizes, of any desired shape and istypically arranged in a loose bed confined within a treating tank bymeans which prevent the escape of the particulate matter but which, atthe same time, permit fluid flow therethrough. Alternatively, techniquesfor adhering the particles into an aggregate porous body with thesurface areas freely exposed can be utilized. Suitable techniques forforming such aggregate porous bodies include sintering and processeswherein a binder is utilized which results in all, or substantially all,of the surface area of the particles freely exposed for contactingfluids to be treated therewith. An important embodiment of the presentinvention is directed to a water treating method which employs metalparticulate matter such as for example aluminum, iron, steel, zinc, andcopper, as well as mixtures and alloys thereof, to provide removal ofundesirable contaminants such as hydrogen sulfide and sulfur dioxide. Inthis regard, an important aspect of the present invention involves adiscovery that such a method will provide economical and long lastingremovable of such undesirable contaminants and thereby greatly eliminatethe weak link in most treatment systems i.e. maintaining and monitoringthe system on a relatively frequent basis.

Another feature of the present invention involves a method of using sucha bed of metal particulate matter in conjuntion with another type offluid treating aparatus such as a reverse osmosis process or anion-exchange process. In this regard, an important aspect of the presentinvention involves the removal of undesireable elements and compoundssuch as chlorine, hydrogen sulfide and sulfur dioxide which may bedetrimental to the operation and life of other treatment methods such asreverse osmosis and ion-exchange processes.

Another feature of the present invention involves adjusting the PH ofthe fluid and subsequently passing it through such a bed of metalparticulate matter. In this regard, an important aspect of the presentinvention involves regulating the pH of the fluid prior to treatment toenhance the removal of contaminants having pH dependentoxidation-reduction activities.

Another feature of the present invention involves the conjoint use ofdual containers having beds of such metal particulate matter arranged inseries with a pH feeder interposed therebetween. Such a method of fluidtreatment allows the user to take advantage of the pH of the sourcefluid at the inlet of the first container to treat the contaminants thatare more responsive to treatment at the original source fluid pH andthen to adjust the pH to treat contaminants which may be moreeffectively treated at another pH value to subsequently treat the fluidagain in the second container.

It is therefore, an important object to the present invention to providean improved fluid treating method.

Another object of the invention is to provide a fluid treating methodwhich is economical to use, which has a relatively long life so as toavoid frequent maintenance and monitoring, and which eliminates the needto regenerate the treating medium and, accordingly, the need to disposeof concentrated contaminants inherent in other conventional treatmentprocesses such as reverse osmosis and ion-exchange processes.

Another object of the invention is to provide a novel method of treatingundesirable constituents such as chlorine, nitrates, hydrogen sulfideand sulfur dioxide present in a fluid such as water withoutconcentrating such constitutents in the treating medium.

Another object of the invention is to provide a fluid treating methodwhich includes treating the fluid by passing the raw fluid containingundesirable constitutents through a bed of metallic particulate mattercharacterized by a redox potential which relative to the redox potentialof the undesirable constituents sought to be treated establishesconditions for spontaneous oxidation and reduction reactions between themetal particulate matter and the undesirable constituents when the fluidis in contact with the metal particles.

Another object of the present invention is to provide an improved methodof treating fluids wherein the fluids are first passed through a bed ofmetallic particulate matter to treat undesirable constituents presentsuch as chlorine which may be harmful to a conventional fluid treatmentprocess such as a reverse osmosis process or an ion-exchange process andto then pass the fluid through such a conventional treatment process.

These objects and other objects and advantages of the invention areaccomplished by providing a method for treating fluid which includespassing fluid containing undesirable elements and compounds through abed of metal particulate matter. The particulate matter is preferablychosen from metals such as aluminump zinc, iron, steel, and copper aswell as mixtures and alloys thereof, having favorable redox potentialsrelative to the undesirable constituents such as chlorine and nitratessought to be treated so as to establish conditions for spontaneousoxidation and reduction reactions between the metal particulate matterand the undersirable constituents when the fluid is in contact with themetal particles.

Although an important aspect of the present invention is directed to thetreatment of water especially drinking water, it will be appreciatedthat the method of this invention may also find advantageous utility inthe treatment of a variety of other source fluids with various differentundesirable contaminants. For purposes of illustration only therefore,this invention will, in most part, be described by reference to anembodiment wherein water is the source fluid being treated.

It has now been discovered that the composition of a given water supplycan be altered with respect to certain contaminants therein such asdissolved chlorine, nitrates, hydrogen sulfide and sulfur dioxide bybringing the water in contact with metals such as aluminum, iron, steel,zinc, and copper as well as mixtures and alloys thereof. For example, ithas been noted that when water containing high concentrations ofdissolved chlorine is passed through a canister housing metallicparticulate matter such as brass that the detectable chlorine level ofthe effluent water is greatly reduced, if not totally eliminated.

It has further been discovered that such a method of fluid treatment isalso effective under certain operating conditions to significantlyreduce and/or eliminate the nitrate concentration of the effluent water.As a result of such findings, the present development has widespreadapplication to the inorganic contaminants hydrogen sulphide and sulphurdioxide.

Moreover it is believed that the useful life of such a method of fluidtreatment under normal operating conditions, would far exceed the usefullife of other conventional treating systems. Accordingly, such a findingrepresents a considerable step forward in the art in that it helps toeliminate one of the major drawbacks of conventional systems, i.e. theneed to frequently replenish the active source of treatment and theconcomitant need to constantly maintain and monitor the system.

In addition such a method has wide spread potential application for avariety of domestic, commercial and industrial uses. For example notingthat chlorine and iodine are effective anti-bacterial agents, drinkingwater, especially in a foreign locale, could be treated by initiallychlorinating or iodizing the water and then the treated water could betransformed to a more palatable and safe form by passing the chlorinatedor iodized water through a portable canister containing metal particlesin accordance with the present invention.

As previously noted, this development is intended to have application toother fluid media besides water treatment including other liquid fluidmedia as well as gaseous fluid media by itself as well as gaseous fluidmedia dissolved in liquids. For example, removal of hazardous gassesespecially the halogens such as chlorine, bromine, and flourine bypassing those gasses through a canister housing a bed of metallic matteris contemplated by, and within the scope of, the present invention. Suchan application may provide an alternate method of purifying contaminatedair such as in a gas mask or may further be used as an alternative to orin conjunction with conventional scrubbing processes.

The method of the present invention contemplates the use of severaldifferent metals as well as mixtures and alloys thereof. It ishypothesized, without being limited to any particular theory of theinvention, that the treatment process of the present invention isaccomplished by spontaneous oxidation-reduction reactions. Accordingly,it is believed that the metal particulate matter should be selected froma group of metals including mixtures and alloys thereof, which arerelatively good redox agents relative to the undesirable constituentssought to be treated so as to establish conditions for spontaneousoxidation and reduction reactions between the metal particulate matterand the undesirable constituents when the fluid is in contact with themetal particulate matter.

The relative tendencies of different species to be reduced or oxidizedcan be predicted from their standard reduction potentials (E° values at25° C.). By comparing the E° values for different species it is possibleto determine whether an oxidation-reduction will spontaneously occur. Inaccordance with the present invention, metals which are relatively goodredox agents relative to the elements or compounds sought to be treatedare those metals which are predicted to react spontaneously with suchelements and compounds.

For example, chlorine dissolved in water having a pH of approximately 7and at 25° C. exists as HOCl and ClO⁻ with HOCl predominating on theacid side and ClO⁻ predominating on the base side. Assuming forsimplicity that ClO⁻ is the reacting species the following redoxreactions are representative of those contemplated by the presentinvention: ##EQU1## As calculated, both zinc and copper should eachreact spontaneously with hypochlorite (ClO⁻) with the zinc theoreticallybeing more spontaneous since it has the more positive potential.

In practice it has been found that a zinc and copper alloy, such asbrass is more effective in the removal of dissolved chlorine than iseither pure zinc or pure copper or a heterogeneous mixture thereof. Inaddition to the noted effectiveness of brass, brass is also a preferredmetal from the viewpoint of chemical safety. This is especially true inaqueous media since brass does not have the violent reactivity toaqueous fluids as do metals such as pure sodium, potasium, calcium orzinc.

Where brass is the chosen metal, it has been found that washing thebrass such as with a hydrochloric acid solution and then rinsing thebrass will cleanse the surface of the brass of contaminants, such asiron filings or other foreign matter, which might interfere with theactivity of the brass. However, it has additionally been noted that thesurface of the brass which is exposed to the atmosphere or to a sourcefluid such as water may develop a greenish rust which may be a carbonateana/or oxide complex. when the surface itself is physically scraped toremove the greenish rust, the removed rust also shows excellentpurifiying tendencies.

Qualitive analysis of water to which chlorine was added and which wastreated by being passed through a bed of brass showed that such treatingconsistently effected a decrease in the amount of chlorine in the water.Set forth below are Examples I and II which describe quantitativeanaylsis conducted by independent laboratories of the composition of thebrass used to treat the water and of the water treated, respectively,both before and after treatment. Analysis of the brass, as described inExample I below, indicated that passing water through the bed of brassdid alter the composition of the brass as might be expected ifoxidation-reduction processes were occurring. As shown in Example IIbelow, the independent laboratory analysis of the influent and effluentwater passed through the bed of brass did confirm the virtualelimination of the chlorine contained in the influent water.

EXAMPLE I

Water was passed through a cylinder housing a 3 inch by 6 inch bed of14×30 mesh brass trapped between screens to prevent the escape of thebrass. The water passed through the brass bed originated from theVillage of Constantine, Michigan water supply which is not chlorinatedbut which contains dissolved nitrates from approximately 10 to 13 partsper million. Amounts of chlorine, from approximately 2 to 13 parts permillion, were introduced into the influent water to test the extent ofdecrease in the chlorine level. After approximately 51,000 gallons ofwater had passed through the bed of brass it was observed that the bedhad diminished in height about one half inch. A fresh sample of brassfrom which the bed was composed was analyzed as was a sample of brasstaken from the bed after approximately 51,000 gallons of water hadpassed therethrough.

Elemental composition of these samples was determined by DirectlyCoupled Plasma-Atomic Emission Spectroscopy using a Beckman SpectraspanVI Spectrometer. Samples were prepared for plasma emission analysis bydissolving 0.1000 grams into 20 milliliters of a 50/50 concentratednitric acid/distilled water mixture. Total solution weight was thenbrought to 100.00 grams by the addition of distilled water.

Elemental composition was determined as the average of values obtainedfrom the following emission lines for each element: Copper; 213.598 nm.,233.008 nm.; Iron; 238.204 nm., 259.940 nm., 371.994 nm.; Zinc: 213.856nm., 206.200 nm., 202.548 nm.; Lead; 405.783 nm., 283.306 nm., 368.348nm.. The results were:

    ______________________________________                                        BRASS ANALYSIS                                                                BEFORE TREATMENT     AFTER TREATMENT                                          ______________________________________                                        % Copper                                                                              59.2             65.0                                                 % Zinc  35.2             27.8                                                 % Lead  2.5              2.5                                                  % Iron  0.2              0.2                                                  ______________________________________                                    

Emission wavelengths for tin and aluminum were also examined, but theseelements could not be detected at the 1 to 1000 sample dilution.

EXAMPLE II

Two sets of samples of influent and effluent water which had passedthrough the brass bed of Example I after it had been used to treatapproximately 51,000 gallons of water were sent to an independentlaboratory for analysis. Sample Set A was unchlorinated tap watersupplied by the Village of Constantine, Michigan water supply and sampleSet B was tap water to which chlorine was added. The results of theanalysis follow:

    ______________________________________                                        SAMPLE SET A                                                                  PARAMETER     UNITS        IN     OUT                                         ______________________________________                                        Nitrite Nitrogen                                                                            mg/l         10.35  9.34                                        Nitrate & Nitrite                                                                           mg/l         .01    .01                                         Organic Nitrogen                                                                            mg/l         10.35  9.35                                        Aluminum (Al) mg/l         0.5    0.5                                         Copper (Cu)   mg/l         0.04   0.27                                        Iron (Fe)     mg/l         0.05   0.34                                        Potassium (K) mg/l         1.00   1.47                                        Sodium (Na)   mg/l         3.8    5.2                                         Zinc (Zn)     mg/l         0.12   1.3                                         ______________________________________                                    

    ______________________________________                                        SAMPLE SET B                                                                  PARAMETER     UNITS        IN     OUT                                         ______________________________________                                        Chloride      mg/l         29.5   32.0                                        Chlorine      mg/l         13.0   0.1                                         Nitrate Nitrogen                                                                            mg/l         11.35  10.69                                       Nitrite Nitrogen                                                                            mg/l         .01    0.01                                        Nitrate & Nitrite                                                                           mg/l         11.35  10.69                                       Aluminum (Al) mg/l         0.5    0.5                                         Calcium (Ca)  mg/l         93.0   94                                          Copper (Cu)   mg/l         0.05   .26                                         Magnesium (Mg)                                                                              mg/l         24.0   24.4                                        Potassium (K) mg/l         1.02   1.06                                        Sodium (Na)   mg/l         17.1   17.8                                        Zinc (Zn)     mg/l         0.11   4.5                                         ______________________________________                                    

The preceding Examples are offered to illustrate the method of thepresent invention and the effect produced thereby and are not intendedto limit the general scope thereof. As shown best by the results ofSample Set B of Example II the method of the present invention iseffective to remove undesireable contaminants such as dissolvedchlorine. The concentration of cations such as zinc and copper cationsdid increase in the effluent as would be expected if anoxidation-reduction process were taking place. Additionally, it has beenobserved that influent tap water has a pH of approximately 6.9 while theeffluent water passing through the brass bed has a pH of approximately7.2.

As shown by the results of both Sample Sets A and B of Example II thetreatment process also effected a decrease in the level of dissolvednitrates in the water. It has been found that transformation ofdissolved nitrates is enhanced and the concentration of the dissolvednitrates is significantly reduced by the present treatment process whenthe fluid medium is at least slightly acidic such as having a pB of 6.5or less. Therefore if the fluid to be treated is neutral or above andtransformation of dissolved nitrates is desired at an enhanced rate aconventional acid feeder can be incorporated into the water treatmentmethod. Alternatively, if the undesirable constituent is moreeffectively removed in a basic media a conventional base feederpretreatment can be used. Where multiple elements or compounds aretreated requiring different pH values the water to be treated may bepassed through successive beds of metal particulate matter, such asbrass, arranged in series with the appropriate conventional acid or basefeeders interposed therebetween.

The following example was performed in order to demonstrate the use ofthe present process to remove hydrogen sulfide from water.

EXAMPLE 3

Cold tap water at a residence kitchen sink was passed through acontainer placed under the sink containing brass (42 eu. in.) composedof copper (50%) and zinc (50% wt.) . Prior to use the brass wasgranulated to an approximate 60 mesh size. All of the cold water flowingthrough the sink was passed through the brass with complete removal ofthe hydrogen sulfide and after four months the brass was still operablefor the removal of hydrogen sulfide.

It has further been found that the speed and degree of removal ofcontaminants is dependent upon the contact time of the fluid with themetal. Accordingly, increasing the contact surface area of the bed suchas by using a smaller metal mesh will enhance the speed and degree ofremoval. Alternatively, or in conjunction therewith; the fluid flow ratecould be decreased to allow a longer contact period. It has stillfurther been found that supplying oxygen to the fluid or metalparticulate matter such as by bubbling air through the fluid or exposingthe bed of metal particulate matter to the atmosphere can enhance thetreatment process.

It has been found that the mesh size of the metal particulate matter canvery appreciably and still be effective at treating the fluid. Forexample, typical mesh sizes of the metal particulate matter will rangefrom 4 to 400 mesh based on U.S. Standard screen sizes and although meshsizes both above and below this range can be utilized mesh sizesporofrom 4 to 30 mesh usually will be preferred for most applications.It will be appreciated that the metal particulate matter can be suppliedin other alternate forms such as in aggregate porous bodies made byadhering the particulate matter into bodies of any desired shape.Suitable techniques for forming such aggregate porous bodies includesintering and processes wherein a binder is utilized which results inall, or substantially all, of the surface area of the particles freelyexposed for contacting fluids to be treated therewith.

It is contemplated that a 20 inch bed of 14×30 mesh brass housed in acylinder having a 6 inch diameter could accomodate the full pressurewater flow rate of a domestic home user and effectively treat influentchlorinated water for many years without replacing the bed of brass.

In addition to chemically treating undesirable constituents the methodof the present invention also has application to physically filteringundesirable suspended solids. This aspect of the present invention hasparticular application to removing suspended iron from water which ironis present in the water naturally, as a result of pretreatment such asby chlorination, or as a result of reaction with the bed of metallicparticles utilized in the present method. Where the water is pretreatedwith chlorine to treat dissolved iron, the present method will not onlyfilter the resulting suspended iron but also will treat the remainingchlorine in the water. The cannister housing the bed of metalparticulate matter can be periodically backwashed to remove any filteredmatter which has collected in the bed and to declog the bed. However,unlike in other treatment methods such as reverse osmosis andion-exchange methods, such backwashing does not result in the dumping ofconcentrated undesirable constituents.

An alternative embodiment of the present invention is a method forpurification whereby the water is passed through both a bed of metallicparticulate matter such as brass and a conventional treatment processsuch as reverse osmosis or ion-exchange. This could be especiallyadvantageous due to the fact that semipermeable membranes such ascellulose acetate often used in reverse osmosis treatment methods areoften susceptible to degredation by dissolved chlorine as isdivinylbenzene which is often used to cross link ion-exchange resins.Utilization of a bed of brass previous to the reverse osmosis membraneor ion-exchanger could substantially lengthen the life of the membraneor resin. Another alternative embodiment of the present invention is amethod for purification whereby the water is passed through both a bedof metallic particulate matter such as brass and a bed of filtermaterial and/or filter aid such as sand to enhance filtration ofundesirable suspended matter.

It will be appreciated by those skilled in the art that manymodifications and variations may be made without departing from thespirit and scope of the present invention. Accordingly the presentinvention is to be limited in scope only by the appended claims.

What is claimed is:
 1. A long lived low maintenance method for treatingliquid to remove the undesirable constitutants hydrogen sulfide, sulfurdioxide and mixtures thereof, said constituents having a first redoxpotential, said method comprising passing said liquid containing saidconstituents through a bed of metal, said metal comprising copper andzinc having a sufficient surface area and a second redox potential suchthat relative to said first redox potential conditions are establishedfor spontaneous oxidation and reduction reactions between saidundesirable constituents and said metal when said liquid is in contactwith said metal.
 2. The method of claim 1 wherein said zinc and coppermetals are in alloy form.
 3. The method of claim 2 wherein said alloy isa brass alloy.
 4. The method of claim 1 wherein said copper and zinc aresintered into a porous body.
 5. The method of claim 1 wherein said metalcomprises metal particles and said particles have a mesh size rangingfrom about 4 to about 400 mesh based on U.S. Standard screen sizes. 6.The method of claim 5 wherein said mesh size ranges from about 4 toabout 30 mesh.
 7. The method of claim 5 wherein said liquid is water andsaid metal particles are brass metal particles.
 8. The method of claim 1wherein said liquid is water and said method further comprises the stepof adjusting the pH of said water to a desired level prior to passingsaid fluid through said bed of metal.
 9. The method of claim 1 whereinsaid method further comprises the step of supplying oxygen to saidmetal.
 10. The method of claim 9 wherein said oxygen is supplied to saidmetal by aeration.
 11. The method of claim 1 wherein said liquid iswater and said method further comprises the step of passing said treatedfluid through a conventional treatment process selected from the groupconsisting of activated carbon, ion-exchange, and reverse osmosisconventional treatment processes.
 12. The method of claim 1 wherein saidliquid is water and said method further comprises the step of passingsaid treated liquid through a filtration medium.
 13. The method of claim12 wherein said filtration medium is sand.